Substances to stimulate the extraction of crudeoil and a method of processing them

ABSTRACT

Substances to stimulate the extraction of crude oil and a method, of processing them: This invention is about substances to stimulate the extraction of crude oils, especially the ponderous and paraffin one, not clogging the route and the abutting deposits of the oil derrick by changing the deposit&#39;s reology and also about solubility of the aggregates which were made from paraffin resins on the oil derrick&#39;s circulation route, using a similar chemical vector to the prodrugs from the medicine industry. The substance to stimulate the extraction of crude oil by increasing the fluidization characterized by the fact that 90% from the volume is made by mixing three fractions oil types from the distilled mineral coal: −20-30% phenol oil (fraction distilled from 170-190° C.), −20-40% absorption oil (fraction distilled from 250-270° C.); −20-40% polymerized oil (fraction distilled from 320-350° C.); which is called chemical vector and till 100% is completing itself with organic reactive like solvents, active-tensioned substances, generating gas substances.

This invention is about substances to stimulate the extraction of crude oils, especially the ponderous and paraffin one, not clogging the route and the abutting deposits of the oil derrick by changing the deposit's reology and also about solubility of the aggregates which were made from paraffin resins on the oil derrick's circulation route, using a similar chemical vector to the podrugs from the medicine industry.

There are substances which are destined not to clog the extraction pipe that are especially formed by three types:

water detergents emulsions

refined oil solvents

substances which were obtained by coke's distilling

It is already known that crude oil has an advanced composition (from easily volatile fraction, solvents, gasoline, to the by paraffin's and asphaltenes which are known, by the generic name, as “Godeville wax”).

Working with the oil-derrick generates local changes of pressures and different temperature sections, enough to form local deposes and, also, final opturates, which are made to stop or to burden the fluid phase's circulation on the crude oil by the circulation tubes (columns and tubing).

An increase in thickness of the crude oil is also producing in the deposit, in the abutting area, around the oil-derrick and that come in the long run from the extraction of the fluid phase; the thickness of the stratum is from 10-15 cm to 1-2 m and is made from paraffin systems of swarms which are narrowing the afflux of the fluid phase to the oil-derrick's pomp. There are processes and methods already known, that lead to the diminishing of these effects by using some chemical solvents solutions or watery detergents solutions which allow the liquefaction of the area abutting the oil-derrick and facilitate the leaking of the fluid phase.

The chemical-solutions which-use organic solvents are disadvantaged by the fact that they have 0.6-0.8 gr/cm³ density and that leads to the fact that, being set free from the oil-derrick's perforations in the abutting area, they grow to the higher part, meaning that not perforating area of the oil-derrick, and they are not activate in the working area.

Watery detergents solutions act by flowing out, down the deposit, having 1 gr/cm density (higher than the crude oil's density), only that, these new created intern faces are not covered by a blister and paraffin are just as much active as others, so they complete the paraffin swarms, after the watery detergent solutions passing by.

On the other half, the water that was let in maintains itself neutral and this is not to be found like useful fraction in the extraction, meanwhile the coal oil, that was propose as chemical vector in order to form the solutions, can be processed in refineries and that way it improves the distilled one by cyclical valuable fractions.

So, because of the coal oil's condensed cycles failure, it can reach to ecological gasoline, which has an octane number that was been grown up directly from the refinery, if the oil percent that brings the crude oil in the refinery had been corrected.

This invention solves a technical problem: to perform a new composition for stimulating the oil extraction, which is build by fractions from the distilled coals, improved by solvents, detergents, acids, alkali, generating salts like ammonium salts and all of them have a superior effect in stimulating the extracting and improving the flowing reology.

That invention has a special ecological compound meaning that it proposes an excellent method for processing and extending (expanding) of some pollution substances which are very intense, like naphthalene, anthracene and, also, other creosols, by their extinction into the oil deposit and by changing them in useful compounds, using “in situ” reactions.

Any draining technology of those polluting substances on the Earth face is so much more polluting than the extinction into the oil deposit, without some other material or energetically consuming.

The oil that had been chosen is composed by the combination of coke-oven coal's distilled fractions, according to this invention, must have 1.15-1.17 gr/cmc density in order to be a perfect vector for the already formed solutions. This means that the creosote or impregnation oil's fractions may be chosen, but this choice refers also to the polymerized oil, so that their mixture must discharge the chemical vector condition.

The main substances, which was build as a chemical vector, is formed by three fractions, obtained from the coke oven distilled coal oil, just the way they were defined by STAS 3261/87 and presented from the boiling point's point of view the typical weight and most chemical composition, already being known that by industrial distillation can be produced such mixtures:

1 fraction-is composed from what is called (technical name) “phenol oil”; it has 170-190° C. as distillation maximum and minimum, 1.15-1.2 g/cm³ density and it contains, in the first place, creosol, naphthalene and anthracene with some free radicals, all by the main formula;

2 fraction-is composed from what is called (technical name) “absorption oil” (by STAS 3362); it has 250-270° C. as distillation maximum and minimum, 1.19-1.122 g/cm³ density and it also contains phenanthene, fluorene, carbazole, fluoranthene;

3 fraction-that is also called (technical name)“polymerized oil”; it has 320-350° C. as distillation maximum and minimum, 1.20-1.23 g/cm³ density and it is chemically composed from acenaphthene and christen;

That composition, composed from 30% from 1 fraction solution-phenol oil mixed with 30% from 2 fraction-absorption oil and all mixed with 30% from 3 fraction, that is also called (technical name) “polymerized oil” is, in fact, the main solution named “chemical vector”, completed by another supplement of 10% meaning types of substances brought from outside the distillation process and called “the vector's charging”

The major chemical substance, so it was called as “chemical vector”, contains numerous substances which can be characterized as very intense pollution compounds and it comes from the coal distillated substances and has the generic name of “mineral coal oil”, according to the invention. The chemically compound of the mineral coal oil is very opened wide and it depends on the processed coal's quality and on the coke-oven technology of the producing factory. By taking over the chemical analyses from more mineral coal oil gorge and ignoring the compounds which have a under 2% weight, we can learn that the following one are really important:

Gas Analysis

compound weight naphthalene 10-14% acenaphthene  8-10% fluorene 16-20% fluoranthene 8-9% pyrene 10-12% antracen  8-12%

Each fraction has an important role in the physical and chemical behavior of the chemical vector comparing the crude oil and the paraffin systems that it contains.

phenol oil has an important role in penetrating the paraffin systems, is also a proper solvent and has a higher density than water has;

absorption oil creates inert areas that are incompatible (from the chemical point of view) with the paraffin systems, so these one are not pasting, just like in the solvents case. In crude oil, these are maintaining active areas between paraffin systems (paraffin swarms) which are reuniting them by increasing the paraffin swarm

the generating gas substances, like the ammonium salts (sulfate and carbonate), which must decompose under 70° C., gas that will radically change the reology of crude oil leaking

detergents and tension active substances which (by 2% of the volume or 20% of the chemical charging total) will stabilize the new reology route and will improve the leaking of the paraffin systems, also separating them from the inorganic stage.

The processing structure is formed by the chemical vector (a mixture from the three oils, in a 1:1:1:percent), chemically charged with a 10% plus per volume for solvents, detergents and gas generating substances, and must have, in the end a 1.10-1.12 g/cm³ density.

According to this invention, the treating process refers to the fact that the structure is liable to pressure, in fact, under the extraction tubes, which are blocked down, or in the deposit, even if the flowing flux had been seriously decreased, until it reached a level of pression like 70-80 bars (which is the highest value of the tubes pression/column/tubing, and in that case in which the unlocking is not the very suitable, the pression must be conserved for 4-8 hours and the treatment should be done again, if a major decrease of the pressure is not registered, which would mean that the circuit is unblocked. According to the invention, the structure and the process have the following advantage:

it had been used a solution which can pass by a useful material inside the refinery process;

the high efficiency because its chemical vector character which was constituted when the mixture was formed;

the solution is accessible and using it meaning a medium security aspect because the oil is not used on the land surface, where can appear major pollution effects;

the reduction of the intervention rhythm at the oil-derricks because a longer time for proceeding solution;

there is no need for special equipment for making the treatments;

it has no uncalled secondary effects (metallic corrosion or a emulsifying of the valuable constituents) from crude oil;

from the oil solution used in injection at the refinery are obtained gasoline with a higher octane number and semicircular coke.

According the invention, here is an example for making a substance and also one for making the processing:

EXAMPLE NR. 1

The substance of the treatment network which uses equipment for the stratum technological injection and also the one that is used for broaching the column network has the following volume percent:

30% phenol oil from the first fraction

30%/volum absorption oil

20% polymerized oil

20% ammonium carbonate

etoxiled noniphenol with 5 to 9 grouping etoxys in a 5% percent

3% phenol

At the oil-derrick, which have a low afflux and, also, are presenting a blocking because of the paraffin deposes which exist on the perforating level or on the column's tubes, a unblocking treatment must be done, by using the solution that was presented before, on a percent of 5 mc/solution/perforated meter or, in other case, like blocking the columns to a maximum pressure limited by the tube material 70-90 bars until the route is unblocked. If a improved circulation is not noticed after 5-8 hours, the solution must be taking out by scavenging into the hub and the treatment must be restored until the oil-derrick is efficiently unblocked.

Using a lab analyze, other type of coal oils can be chosen, from their distilling, but only if the typical density passes over 1.08, and the formed vector charges with reactive (solvents, detergents, etc), by the initial purpose and by the characteristics of the deposit. 

1. Composition for treating crude-oils, characterized in that it comprises 20 . . . 30% by volume of phenolic oil which is a distillation fraction having a distillation temperature range from 170-190° C.; 20 . . . 40% by volume of absorption oil which is a distillation fraction having a distillation temperature range from 250 to 270° C.; 20 . . . 40% by volume of polymerization oil which is a distillation fraction having a distillation temperature range from 320 to 350° C., and a mixture of chemical additives for the remainder up to 100% by volume, said mixture containing a surfactant, a gas generator, an acidic substance and a solvent, the density of the composition being of 1.10 . . . 1.12 g/cm³.
 2. Composition according to claim 1, characterized in that the volumetric ratio of the phenolic oil, absorption oil and polymerization oil being preferably of 1:1:1.
 3. Composition according to claim 1, or claim 2, characterized in that the phenolic oil preponderantly comprises cresols, naphthalenes and anthracenes with various chemical radicals attached thereto and has a density of 1.15 . . . 1.20 g/cm³; the absorption oil preponderantly containing phenanthrene, fluorene, carbosols and fluoranthrene and has a density of 1.19 . . . 1.22 g/cm³, and the polymerization oil preponderantly contains pyrene, acenaphthenes and chrysenes, and has a density of 1.20 . . . 1.23 g/cm³.
 4. Composition according to claim 1, characterized in that the mixture of chemical additives preferably consists of 25% by weight of surfactant, preferably nonylphenol ethoxylated with 5 . . . 9 ethoxy groups; 10% by weight of gas generating substance, preferably consisting of ammonium salts selected from ammonium sulphates or carbonates which are decomposed at a temperature less than 70° C. causing the generation of gases; 15% by weight of an acidic substance, preferably phenol and solvent for the remainder to 100%.
 5. Composition according to claim 1 and claim 4, characterized in that it comprises 30% by volume of phenolic oil, 30% by volume of absorption oil, 20% by volume of polymerization oil and 20% by volume of chemical additive mixture comprising 10% by weight of ammonium carbonate, 25% by weight of nonylphenol ethoxylated with 5-9 ethoxy groups, 15% by weight of phenol and solvent for the remainder to 100%.
 6. Process for treating crude-oils, which is applied by the use of the composition according to claim 1, characterized in that a composition defined in claim 1 is injected under a pressure preferably having a value of 70 . . . . 90 bar through a tubing or through a production casing for crude-oil exploitation through a well which penetrates and opens a productive crude oil-field, followed by ceasing the fluid extraction through the tubing for 4 . . . 8 hours and thereafter the well is started up.
 7. Process according to claim 6, characterized in that in the tubing or in the production casing there is injected an amount of the composition defined in claim 1 which should ensure a distribution preferably of 5 m³ of solution/meter of perforated tubing portion.
 8. Process for treating crude-oils, which is applied by the use of the composition according to claim 1, carried out in another variant, characterized in that a composition according to claim 1 is injected through a line for conveying the crude-oil extracted through a well, in case of blocking the flow therethrough, the injection being carried out with a maximum pressure value which is limited by the pressure that the tubing can withstand, and the pressure value is maintained for 4 . . . 8 hours within the line.
 9. Process for treating the crude-oils according to claim 6 or claim 8, characterized in that, in the situation in which after 4 . . . 8 hours the crude-oil circulation is not restored to the normal parameters, the composition injected into the tubing or in the line is extracted and then the composition according to claim 1 is injected again. 